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Transport Phenomena.pdf

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406 Chapter 12 Temperature Distributions with More Than One Independent Variable<br />

12D.7. Asymptotic solution for small z for laminar tube flow with constant heat flux. Fill in the<br />

missing steps between Eq. 12.2-23 and Eq. 12.2-24. Insertion of the expression for ф into Eq.<br />

12.2-23 gives<br />

в =<br />

J<br />

x LI (3) J x<br />

Why do we introduce the symbols J and ~x>Next, exchange the order of integration to get<br />

@ = ^9X Г UL f * Jexpf-pW*) \dx<br />

J<br />

X [Л\з) J x J<br />

(12D.7-2)<br />

Then perform the integration over x and obtain<br />

в(г>' A) = Щ-1 ex P(~^3) ~ Ц J o<br />

" ^ exp(-^3) ^ - ^ x exp(-^3<br />

) rf^J I (12D.7-3)<br />

Then use the definitions T(a) = f% 1 а ~^е~ 1 &\ and T(a, x) = /J F~ A e~ [ dt for the complete and incomplete<br />

gamma functions.<br />

12D.8. Forced conduction heat transfer from a flat plate (thermal boundary layer extends beyond<br />

the momentum boundary layer). Show that the result analogous to Eq. 12.4-14 for A > 1 is 13<br />

3<br />

H. Schlichting, Boundary-Layer Theory, 7th edition, McGraw-Hill, New York (1979), p. 306.

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